CN217119376U - Novel separate extraction crystallization crystal growing tank - Google Patents
Novel separate extraction crystallization crystal growing tank Download PDFInfo
- Publication number
- CN217119376U CN217119376U CN202123207081.7U CN202123207081U CN217119376U CN 217119376 U CN217119376 U CN 217119376U CN 202123207081 U CN202123207081 U CN 202123207081U CN 217119376 U CN217119376 U CN 217119376U
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- Prior art keywords
- stirring
- shaft
- stirring shaft
- tank body
- tank
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- Expired - Fee Related
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- 239000013078 crystal Substances 0.000 title claims abstract description 23
- 238000002425 crystallisation Methods 0.000 title claims abstract description 17
- 230000008025 crystallization Effects 0.000 title claims abstract description 17
- 238000000605 extraction Methods 0.000 title abstract description 4
- 238000003756 stirring Methods 0.000 claims abstract description 57
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000005194 fractionation Methods 0.000 claims description 7
- 238000009434 installation Methods 0.000 claims description 2
- 238000002156 mixing Methods 0.000 abstract description 17
- 239000000463 material Substances 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 7
- 239000004519 grease Substances 0.000 description 3
- 238000010907 mechanical stirring Methods 0.000 description 3
- 230000003450 growing effect Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model provides a novel separate extraction crystallization crystal growing tank, the inside of the tank body is provided with a stirring shaft and stirring blades, the stirring shaft is a hollow rigid shaft, the stirring blades are composed of a plurality of hollow pipes communicated by the stirring shaft, the hollow pipes are longitudinally and symmetrically distributed, the upper end and the lower end of the stirring shaft are rotatably connected with the tank body, the upper end of the stirring shaft is positioned outside the tank body and is communicated with a water inlet pipe, the lower end of the stirring shaft is positioned outside the tank body and is communicated with a water return pipe, the water inlet pipe is connected with a water pump, and the water return pipe is connected with a water tank; the stirring shaft is driven by a stirring motor, and the stirring motor is arranged on the upper part of the tank body through a motor bracket. The beneficial effects are as follows: set up the stirring leaf of symmetric distribution in the crystallizer, can drive the material that is close to the (mixing) shaft when the stirring, though the material rotational angle who is close to the (mixing) shaft can be less than the material of keeping away from the (mixing) shaft, but the efficiency of the hollow tube heat transfer that is close to the (mixing) shaft has obtained the improvement, has improved the effect of crystal growing.
Description
Technical Field
The utility model relates to a crystallization crystal growing tank, in particular to a novel fractionation crystallization crystal growing tank.
Background
The crystallization and crystal growth tank is characterized in that a mechanical stirring shaft and stirring blades thereof are arranged in the center of a tank body, and a coil pipe for heat exchange and temperature reduction is arranged between the tank body and the stirring blades; low-temperature refrigerant liquid flows through the tank body jacket and the coil pipe; the grease in the tank forcibly flows under stirring, thereby realizing heat exchange and temperature reduction, separating out crystals in the temperature reduction process, and further leading the separated fine crystals to be combined into coarse aggregates. The grease is forced to flow under mechanical stirring to complete the crystallization and crystal growing process.
The oil crystallization crystal growing tank in the prior art has the defects that the linear velocity of the flow of the oil which is stirred by the mechanical stirring blade and is close to the center is low, and the linear velocity is high when the oil is far from the center; the oil in the center area of the tank has little heat exchange and low flow velocity, while the oil in the wall area of the tank has much heat exchange and high flow velocity, so that the crystallization and crystal growth effects of the oil are poor; simultaneously, occupy jar body center by (mixing) shaft and stirring paddle leaf thereof, force the cryogenic liquid coil pipe can not distribute at the center, and the coil pipe is narrow position and in small quantity to the tank shell, makes the crystallization crystal growing effect variation that the grease cooling is inhomogeneous to lead to.
SUMMERY OF THE UTILITY MODEL
The utility model provides a novel separate-extraction crystal growing tank for solving the problems existing in the prior art.
The technical scheme of the utility model is realized like this:
a novel fractionation crystallization crystal growing tank comprises: the tank body is of a double-layer heat insulation structure, a stirring shaft and stirring blades are arranged in the tank body, the stirring shaft is a hollow rigid shaft, the stirring blades are composed of a plurality of hollow pipes communicated with the stirring shaft, the hollow pipes are longitudinally and symmetrically distributed, the upper end and the lower end of the stirring shaft are rotatably connected with the tank body, the upper end of the stirring shaft is positioned outside the tank body and communicated with a water inlet pipe, the lower end of the stirring shaft is positioned outside the tank body and communicated with a water return pipe, the water inlet pipe is connected with a water pump, and the water return pipe is connected with a water tank; the stirring shaft is driven by a stirring motor, and the stirring motor is arranged on the upper part of the tank body through a motor bracket.
Preferably, the ends of the hollow pipes are connected to a transverse pipe, and the stirring shaft is connected and communicated with the transverse pipe.
Preferably, an upper inlet and a lower outlet are further arranged on the double-side heat-insulating outer wall of the tank body.
Preferably, the upper end and the lower end of the stirring shaft are respectively provided with a rotary pipe joint, the pipe joints are rotatably connected with the stirring shaft, and the pipe joints are fixedly connected with the water pipe joints at the end parts of the water inlet pipe and the water return pipe.
The beneficial effects are that:
1. the symmetrically distributed stirring blades are arranged in the crystal growing tank, so that materials close to the stirring shaft can be driven during stirring, and although the rotating angular speed of the materials close to the stirring shaft is lower than that of the materials far away from the stirring shaft, the heat exchange efficiency of the hollow tube close to the stirring shaft is improved, and the crystal growing effect is improved;
2. the crystal growing tank adopts a double-layer heat-insulating tank body, so that the influence of the external temperature on the interior of the tank body can be reduced as much as possible, an upper inlet and a lower outlet are arranged on the tank body, and low-temperature liquid can be introduced into the outer wall of the tank body through the two ports to exchange heat with materials in the tank body;
3. the (mixing) shaft sets up to hollow structure, makes it can also let in low temperature liquid through the inlet tube of tip when rotatory, makes the stirring leaf at (mixing) shaft middle part have good heat transfer effect, provides the efficiency of crystallization.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without any creative effort belong to the protection scope of the present invention.
As shown in fig. 1, a novel fractionation crystallization crystal growing tank comprises: the jar body 1, the support 2 of the installation jar body 1, jar body 1 adopts double-deck thermal-insulated structure, the inside of jar body 1 is equipped with (mixing) shaft 11 and stirring leaf, the (mixing) shaft 11 is the cavity rigidity axle, the stirring leaf comprises many hollow tubes 12 of (mixing) shaft 11 intercommunication, the vertical even symmetric distribution of hollow tube 12, the tip of hollow tube 12 all is connected to violently managing 13 on, the (mixing) shaft 11 with violently manage 13 and be connected and communicate, agitator motor 9 passes through motor support 2 and installs on the upper portion of the jar body 1, the (mixing) shaft 11 is driven by agitator motor 9.
Both ends and jar body 1 rotatable coupling about the (mixing) shaft 11, the (mixing) shaft 11 upper end is located jar body 1 outside and communicates with inlet tube 6, the (mixing) shaft 11 lower extreme is located jar body 1 outside and communicates with wet return 5, inlet tube 6 is connected with water pump 4, wet return 5 is connected with water tank 3, water pump 4 squeezes into (mixing) shaft 11 and stirring leaf with low-temperature liquid from inlet tube 6 in, low-temperature liquid is in jar internal heat absorption back from (mixing) shaft 11 lower part through wet return 5 backward flow in water tank 3, water tank 3 can adopt self to have refrigeration plant's seal box.
An upper inlet 14 and a lower outlet 15 are also arranged on the heat-insulating outer walls at the two sides of the tank body 1, and low-temperature liquid can be introduced into the outer wall of the tank body 1 through the two ports to exchange heat with the materials in the tank body 1; or one of the openings is blocked, and the outer wall is vacuumized to be used as a heat insulation barrier.
The upper end and the lower end of the stirring shaft 11 are respectively provided with a rotary pipe joint 8, the pipe joints 8 are rotatably connected with the stirring shaft 11, the pipe joints 8 are fixedly connected with water pipe joints 7 at the end parts of the water inlet pipe 6 or the water return pipe 5, the water pipe joints 7 and the water pipe cannot rotate, the pipe joints 8 and the stirring shaft 11 are connected in a rotary sealing mode, and the water pipe cannot rotate along with the rotation of the stirring shaft 11.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (4)
1. A novel fractionation crystallization crystal growing tank comprises: jar body, installation the support of the jar body, the jar body adopts double-deck thermal-insulated structure, its characterized in that: the stirring shaft is a hollow rigid shaft, the stirring blades consist of a plurality of hollow pipes communicated with the stirring shaft, the hollow pipes are longitudinally, uniformly and symmetrically distributed, the upper end and the lower end of the stirring shaft are rotatably connected with the tank body, the upper end of the stirring shaft is positioned outside the tank body and is communicated with a water inlet pipe, the lower end of the stirring shaft is positioned outside the tank body and is communicated with a water return pipe, the water inlet pipe is connected with a water pump, and the water return pipe is connected with a water tank; the stirring shaft is driven by a stirring motor, and the stirring motor is arranged on the upper part of the tank body through a motor bracket.
2. The novel fractionation crystallization crystal growing tank according to claim 1, characterized in that: the end parts of the hollow pipes are connected to a transverse pipe, and the stirring shaft is connected and communicated with the transverse pipe.
3. The novel fractionation crystallization crystal growing tank according to claim 1, characterized in that: and the heat-insulating outer walls at two sides of the tank body are also provided with an upper inlet and a lower outlet.
4. The novel fractionation crystallization crystal growing tank according to claim 1, characterized in that: the upper end and the lower end of the stirring shaft are respectively provided with a rotary pipe joint, the pipe joints are rotationally connected with the stirring shaft, and the pipe joints are fixedly connected with water pipe joints at the end parts of the water inlet pipe or the water return pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123207081.7U CN217119376U (en) | 2021-12-20 | 2021-12-20 | Novel separate extraction crystallization crystal growing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123207081.7U CN217119376U (en) | 2021-12-20 | 2021-12-20 | Novel separate extraction crystallization crystal growing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217119376U true CN217119376U (en) | 2022-08-05 |
Family
ID=82616868
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123207081.7U Expired - Fee Related CN217119376U (en) | 2021-12-20 | 2021-12-20 | Novel separate extraction crystallization crystal growing tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217119376U (en) |
-
2021
- 2021-12-20 CN CN202123207081.7U patent/CN217119376U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220805 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |